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EP0955297A1 - Un procédé amélioré pour la préparation des statines - Google Patents

Un procédé amélioré pour la préparation des statines Download PDF

Info

Publication number
EP0955297A1
EP0955297A1 EP98123252A EP98123252A EP0955297A1 EP 0955297 A1 EP0955297 A1 EP 0955297A1 EP 98123252 A EP98123252 A EP 98123252A EP 98123252 A EP98123252 A EP 98123252A EP 0955297 A1 EP0955297 A1 EP 0955297A1
Authority
EP
European Patent Office
Prior art keywords
reaction
lactonization
statins
acid
solvent
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP98123252A
Other languages
German (de)
English (en)
Other versions
EP0955297B9 (fr
EP0955297B1 (fr
Inventor
Yatendra Kumar
Rajest Kumar Thaper
S.M. Dileep Kumar
Jag Mohan Khanna
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ranbaxy Laboratories Ltd
Original Assignee
Ranbaxy Laboratories Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from US09/064,285 external-priority patent/US5917058A/en
Application filed by Ranbaxy Laboratories Ltd filed Critical Ranbaxy Laboratories Ltd
Publication of EP0955297A1 publication Critical patent/EP0955297A1/fr
Application granted granted Critical
Publication of EP0955297B1 publication Critical patent/EP0955297B1/fr
Publication of EP0955297B9 publication Critical patent/EP0955297B9/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D309/00Heterocyclic compounds containing six-membered rings having one oxygen atom as the only ring hetero atom, not condensed with other rings
    • C07D309/16Heterocyclic compounds containing six-membered rings having one oxygen atom as the only ring hetero atom, not condensed with other rings having one double bond between ring members or between a ring member and a non-ring member
    • C07D309/28Heterocyclic compounds containing six-membered rings having one oxygen atom as the only ring hetero atom, not condensed with other rings having one double bond between ring members or between a ring member and a non-ring member with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
    • C07D309/30Oxygen atoms, e.g. delta-lactones

Definitions

  • Lovastatin and its analogs are potent antihypercholesterolemic agents that function by limiting cholesterol biosynthesis by inhibiting the enzyme HMG-CoA reductase.
  • statins which may be referred to,generally as statins, are known to exist in open ring hydroxy acid and also in lactone form.
  • the lactone form and the hydroxy acid form of these compounds have the following general structural Formulas: wherein Z is hydrogen, a metal cation, such as sodium or potassium, or NH 4 , and R is wherein R 1 is H or CH 3 .
  • statins The open hydroxy acid form of the statins (Formula II) is the one which is biologically active. However, the statins are generally administered to a patient in the lactone form (Formula I), which is converted to its active metabolite, the hydroxy acid form, in the body.
  • U.S. patent No. 4,916,239 discloses another process wherein the lactonization reaction is carried out at room temperature by treating the free hydroxy acid ammonium salt of a mevinic acid in a mixture of acetic acid and water, and in the presence of a strong acid catalyst. After the free hydroxy acid-lactone equilibrium is established (reaction has proceeded to 50% conversion), water is gradually added in lots to effect crystallization of the lactone from the reaction medium. This removal of lactone continuously shifts the equilibrium to the lactone side thus leading to reaction completion.
  • This process suffers from several disadvantages and is also not convenient to operate at a large scale for a variety of reasons, some of which are discussed below
  • a strong mineral or an organic acid catalyst e.g., formic, phosphoric, trifluoroacetic, sulphuric, hydrochloric, p-toluene sulphonic, methanesulphonic acids, etc.
  • a strong mineral or an organic acid catalyst e.g., formic, phosphoric, trifluoroacetic, sulphuric, hydrochloric, p-toluene sulphonic, methanesulphonic acids, etc.
  • the excess acid catalyst which is used needs to be neutralized by adding a strong base before filtration of the product.
  • the aim of the present invention is to provide an efficient method for lactonization of statins which method avoids the use of strong corrosive acids and drastic heat conditions and gives a lactonized product of high purity and yield.
  • the present invention provides a novel process for converting the HMG-CoA reductase inhibitors, e.g., the open hydroxy acid forms of lovastatin, simvastatin, and analogs thereof, into their lactone forms, and is convenient to operate on an industrial scale. It allows the lactonizaion reaction to proceed at moderate temperatures without the use of industrially unsafe strong acids.
  • HMG-CoA reductase inhibitors e.g., the open hydroxy acid forms of lovastatin, simvastatin, and analogs thereof
  • the process of this invention comprises treating the open hydroxy acid of the statins, preferably in their salt form, most preferably in their ammonium salt form with acetic acid and in the absence of a strong acid catalyst, under inert anhydrous conditions and at ambient to moderate temperatures.
  • a strong acid is generally regarded as an acid having pK a ⁇ 0).
  • the lactonization reaction proceeds without the addition of strong acid catalysts (as in the prior art), is clean and fast, thus allowing less chance for impurity formation.
  • the lactonized product generally having high solubility in acetic acid, is isolated in pure form after completion of reaction by the addition of an anti-solvent which has the ability to crystallize out the lactonized product.
  • the anti-solvent is selected from water, hexane, heptane, cyclohexane, etc., preferably water, hexane or cyclohexane, most preferably, water.
  • lactonization is an equilibrium reaction
  • the reaction by-product ammonia is consumed in situ by the acetic acid, which is present in excess in the reaction medium, to generate ammonium acetate.
  • the latter being hygroscopic in nature, has a tendency to absorb water, which is also formed as a by-product during the lactonization reaction. There is, therefore, provided a mechanism which allows in situ removal of ammonia and water thereby driving the lactonization reaction to completion.
  • the rate of lactonization is very high and allows the reaction to be completed in a very short period and the lactone product is obtained in high yields and high purity.
  • the reaction is carried out at a temperature from ambient temperature to about 55°C, preferably at about 25-45°C, most preferably at about 35-40°C.
  • the amount of acetic acid is at least about 1 part by volume per part of the starting salt material.
  • Higher amounts of solvent and generally up to about 20 parts by volume may be used.
  • the solvent is in the range of about 3 to 7 parts by volume.
  • the reaction will typically be accomplished within about 3-5 hrs. However, length of time will vary depending on such factors as total volume of solution, temperature of the reaction and the substrate involved.
  • Major advantages of the present invention as compared to the prior art procedures are cost effectiveness, less cumbersome workup, high yield, increased process productivity, clean and environmentally friendly operations.
  • the level of impurity profile, especially for the starting acid and the dimer, are greatly reduced as compared to earlier reported processes.
  • the product which is in the form of a homogenous slurry makes the filtration operations at large scale very easy and workup involves no neutralization step prior to filtration.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Pyrane Compounds (AREA)
  • Saccharide Compounds (AREA)
  • Glass Compositions (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
EP98123252A 1998-04-22 1998-12-07 Un procédé amélioré pour la préparation des statines Expired - Lifetime EP0955297B9 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US09/064,285 US5917058A (en) 1997-10-28 1998-04-22 Process of lactonization in the preparation of statins
US64285 1998-04-22

Publications (3)

Publication Number Publication Date
EP0955297A1 true EP0955297A1 (fr) 1999-11-10
EP0955297B1 EP0955297B1 (fr) 2004-04-21
EP0955297B9 EP0955297B9 (fr) 2004-12-15

Family

ID=22054869

Family Applications (1)

Application Number Title Priority Date Filing Date
EP98123252A Expired - Lifetime EP0955297B9 (fr) 1998-04-22 1998-12-07 Un procédé amélioré pour la préparation des statines

Country Status (10)

Country Link
EP (1) EP0955297B9 (fr)
AT (1) ATE264849T1 (fr)
DE (1) DE69823333T2 (fr)
DK (1) DK0955297T3 (fr)
ES (1) ES2217485T3 (fr)
HK (1) HK1023572A1 (fr)
HU (1) HUP9802936A3 (fr)
PT (1) PT955297E (fr)
RU (1) RU2214407C2 (fr)
ZA (1) ZA9810764B (fr)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002094804A1 (fr) * 2001-05-18 2002-11-28 Aurobindo Pharma Limited Procede permettant la lactonisation pour la production de simvastatine
EP1288212A1 (fr) * 2001-08-27 2003-03-05 CHEIL JEDANG Corporation Procédé de lactonisation dans la préparation de statins
US6573385B1 (en) 1999-11-11 2003-06-03 Biocon India Limited Process for manufacturing simvastatin and novel intermediates thereof
US6573392B1 (en) 1999-11-11 2003-06-03 Biocon India Limited Process for manufacturing simvastatin and the novel intermediates
US6603022B1 (en) 2002-05-10 2003-08-05 Biocon India Limited Process for manufacturing Simvastatin and novel intermediates thereof

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4820850A (en) * 1987-07-10 1989-04-11 Merck & Co., Inc. Process for α-C-alkylation of the 8-acyl group on mevinolin and analogs thereof
US4916239A (en) * 1988-07-19 1990-04-10 Merck & Co., Inc. Process for the lactonization of mevinic acids and analogs thereof
EP0511867A1 (fr) * 1991-05-01 1992-11-04 Merck & Co. Inc. Procédé d'obtention de la simvastatine
US5393893A (en) * 1993-11-08 1995-02-28 Apotex, Inc. Process for producing simvastatin and analogs thereof

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4820850A (en) * 1987-07-10 1989-04-11 Merck & Co., Inc. Process for α-C-alkylation of the 8-acyl group on mevinolin and analogs thereof
US4916239A (en) * 1988-07-19 1990-04-10 Merck & Co., Inc. Process for the lactonization of mevinic acids and analogs thereof
EP0511867A1 (fr) * 1991-05-01 1992-11-04 Merck & Co. Inc. Procédé d'obtention de la simvastatine
US5393893A (en) * 1993-11-08 1995-02-28 Apotex, Inc. Process for producing simvastatin and analogs thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6573385B1 (en) 1999-11-11 2003-06-03 Biocon India Limited Process for manufacturing simvastatin and novel intermediates thereof
US6573392B1 (en) 1999-11-11 2003-06-03 Biocon India Limited Process for manufacturing simvastatin and the novel intermediates
WO2002094804A1 (fr) * 2001-05-18 2002-11-28 Aurobindo Pharma Limited Procede permettant la lactonisation pour la production de simvastatine
EP1288212A1 (fr) * 2001-08-27 2003-03-05 CHEIL JEDANG Corporation Procédé de lactonisation dans la préparation de statins
US6603022B1 (en) 2002-05-10 2003-08-05 Biocon India Limited Process for manufacturing Simvastatin and novel intermediates thereof

Also Published As

Publication number Publication date
ZA9810764B (en) 1999-08-13
EP0955297B9 (fr) 2004-12-15
HU9802936D0 (en) 1999-02-01
RU2214407C2 (ru) 2003-10-20
EP0955297B1 (fr) 2004-04-21
DE69823333D1 (de) 2004-05-27
DK0955297T3 (da) 2004-08-16
HUP9802936A3 (en) 2000-04-28
HK1023572A1 (en) 2000-09-15
PT955297E (pt) 2004-08-31
ES2217485T3 (es) 2004-11-01
DE69823333T2 (de) 2005-04-07
ATE264849T1 (de) 2004-05-15
HUP9802936A2 (hu) 1999-11-29

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